EP0760076B2 - Firing furnace with a revolving firing zone and a cooled internal wall - Google Patents

Firing furnace with a revolving firing zone and a cooled internal wall Download PDF

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Publication number
EP0760076B2
EP0760076B2 EP96901839A EP96901839A EP0760076B2 EP 0760076 B2 EP0760076 B2 EP 0760076B2 EP 96901839 A EP96901839 A EP 96901839A EP 96901839 A EP96901839 A EP 96901839A EP 0760076 B2 EP0760076 B2 EP 0760076B2
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EP
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Prior art keywords
fact
furnace according
ring furnace
ventilation
vertical
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German (de)
French (fr)
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EP0760076B1 (en
EP0760076A1 (en
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François Charmier
Philippe Breme
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Rio Tinto France SAS
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Aluminium Pechiney SA
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    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/515Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics
    • C04B35/52Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on carbon, e.g. graphite
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B13/00Furnaces with both stationary charge and progression of heating, e.g. of ring type or of the type in which a segmental kiln moves over a stationary charge
    • F27B13/02Furnaces with both stationary charge and progression of heating, e.g. of ring type or of the type in which a segmental kiln moves over a stationary charge of multiple-chamber type with permanent partitions; Combinations of furnaces

Definitions

  • the invention relates to a rotary kiln for cooking carbonaceous products and in particular carbon anodes used for the production of aluminum by electrolysis according to the Hall-Héroult process.
  • Rotating fire furnaces such as that described in the European patent application EP-A-0 541 165, generally comprise two parallel rows of juxtaposed rectangular-shaped chambers in which anodes or other green carbonaceous products are fired. These rooms, separated by transverse walls, and whose bottom and side walls are thermally insulated by an insulating brickwork, are subdivided into several compartments or cells containing the products to be cooked. These cells are separated by thin-walled hollow partitions arranged parallel to the major axis of the furnace. In these hollow partitions circulate hot gases, whose temperature can reach 1150 or 1200 ° C. They are formed essentially by the combustion gases generated by one or more burner ramps that are moved from one chamber to the next as the cooking takes place.
  • Rotating furnaces, open-type furnaces and closed-type furnaces are often distinguished.
  • the difference lies mainly in the constructive characteristics of the interior brickwork leading to various paths of the hot gases circulating around the cells containing the loads to be cooked, but the general organization of these rotary kilns remains the same with the existence of 2 rows parallel rooms, whose length can reach nearly 200 meters, connected at their ends by flues.
  • the advantage of the unique casing is its great compactness and therefore the resulting saving of space as well as the savings it entails in terms of investment costs, but this to the detriment of good performance and therefore longevity insulating briquetting which is arranged between the 2 rows of rooms. Indeed, these briquetting bear significant thermal and mechanical stresses due to the amplitude of the temperature variations to which they are subjected and thrusts exerted by the chambers located on either side of these briquetting. Due to the difficulties of ensuring effective cooling of this central zone, the cooling of the single casing is limited in most single-cased industrial furnaces to a simple natural ventilation of the walls or outer walls of the casing. This differential heat treatment of the central zone with respect to the outer zones also generates mechanical and thermal stresses created by the high thermal gradient existing between the chambers facing each other in the two rows of chambers constituting the furnace.
  • the major advantage of the double bowl is that the load constituted by the row of chambers, is treated symmetrically with respect to its longitudinal axis.
  • the inner sails are cooled like the outer sails in the most frequent case where there is a natural ventilation provided in particular by the circulation channels or vaults which cool the bottom of the oven.
  • This configuration therefore makes it possible to extend the lifetime of the briquetting, with, however, the disadvantages of a higher realization cost and a larger footprint with identical production capacity.
  • the invention provides a solution to this problem. It relates more specifically to a rotary fired furnace for cooking carbon products including in particular 2 parallel rows of cooking chambers. placed with their own thermal insulation jointly or separately in a casing, preferably made of concrete, at least cooled by ventilation of its external lateral walls or external walls, characterized in that the 2 parallel rows of cooking chambers are separated by an internal veil which is specifically cooled and made integral with the bottom of the casing or write off.
  • This internal web comprises a network of vertical, horizontal ducts or any other geometry allowing the circulation of a coolant liquid or gaseous, allowing lowering the temperature of the constituent material (s) of the central web to an acceptable value by said materials.
  • the inner web is formed by 2 vertical uprights of identical thickness, symmetrical with respect to the vertical axis of symmetry, linked to their lower ends at the bottom of the casing or raft. These amounts are maintained at fixed spacing by vertical or horizontal spacers so as to create vertical or horizontal corridors in which circulates the cooling fluid, which is preferably ventilation air supplied by appropriate ventilation means.
  • the spacers are made of the same material as the vertical uprights.
  • Suitable means of ventilation include natural ventilation, forced ventilation or mixed ventilation. These ventilation means are grouped together with the other auxiliary means essential for driving the oven, including control and regulation means and lifting and handling means, in the building that houses the oven.
  • FIG. 1 is representative of a rotary firing furnace 1 comprising two parallel rows 2a and 2b of juxtaposed chambers 3 of rectangular shape separated by transverse walls 4 and subdivided into cells 5 containing the product to be fired. These cells are separated by hollow partitions 6 with thin walls parallel to the major axis A, A 'of the furnace in which circulate the gases for heating the charges (not shown) placed in the cells. These hot gases are mainly combustion gases generated by one or more ramps 7 of burners that are moved from one chamber to the next as the cooking of the product takes place.
  • the 2 concrete casings 8a and 8b respectively contain the chambers 3a and 3b with their thermal insulation 17a and 17b.
  • the external sails 9a and 9b as well as the 2 inner sails 10a and 10b of the two casings are cooled by natural ventilation as well as the 2 rafts 12a and 12b equipped with vaults 11a and 11b.
  • the distance between the 2 outer faces of the inner sails is of the order of 2 to 3 meters to allow sufficient ventilation of the two casings by natural draft.
  • the two parallel rows 2a and 2b of chambers 3a, 3b are contained with their respective thermal insulation 17a and 17b in a single casing 8 of concrete formed by 2 outer vertical sails 9a, 9b resting on a concrete base 12 .
  • the frequency of maintenance interventions on the central brickwork is much higher than that observed for brickwork of rooms having their individual casing which, independently of the direct cost of higher maintenance, can lead to a limitation of the capacity. of production.
  • the width reduction of about 3 meters of a single casing kiln compared to a double casing furnace allows a reduction in floor area of 300 to 600 m 2 according to the length of the oven.
  • FIGS. 4 and 5 representative of a ventilated central fan rotating firing furnace of the invention, there are interposed between the thermal insulators 17a and 17b of the chambers 3a and 3b, and more precisely between the central briquetting, a vertical central veil. or inner sail 10, preferably made of concrete, the total thickness of which varies according to the capacity of the furnace and more precisely the importance of the thermal flows to be evacuated, but also the nature of the material used and in particular its thermomechanical properties , crush and thermal shock resistance, thermal conductivity ...
  • This web 10 has a total thickness in its central and upper parts of between 200 and 900 mm and preferably between 400 and 600 mm. It generally widens gradually to its base resting on the casing floor or base 12.
  • the veil 10 made mostly of concrete identical to that of the casing 8, is preferably formed by 2 uprights vertical 13 and 13b of identical thickness, symmetrical with respect to the vertical axis CC '.
  • the spacing between two partitions defined by the vertical or horizontal spacers 15 is between 50 and 500 mm, but preferably between 100 and 300 mm, so as to provide sufficient ventilation in a minimum volume.
  • the spacing of the spacers 15 it is determined according to the deformation stresses to which said amounts are subjected under the effect of particular charges and temperature. This spacing is most often between 0.5 and 1 meter.
  • the inner sail 10 cooled and limited thickness therefore does not lead, all things being equal, significant expansion of the furnace rotating, as is the case with the double-casing furnace.
  • being cooled naturally, or forcibly by ventilation of air, or by any other cooling fluid it makes it possible to recreate the mechanical and thermal symmetry that is lacking in the single vessel.
  • the choice of the ventilation mode depends mainly on the importance of the heat flow to be removed from the central zone of the oven to limit the temperature peaks in the brickwork.
  • a forced ventilation unit powerful enough to inject fresh air, preferably from the bottom to the top of the vertical corridors 16 of the inner veil 10, possibly by the intermediate of the vaults 11 of the raft, and this while maintaining for the outer sails 9a, 9b, a natural ventilation.
  • Forced ventilation can also be performed by injecting fresh air into the horizontal corridors 16, that is to say longitudinally from one end of the inner web 10 to the other end.
  • the injection of fresh air by blowing or aspiration is carried out using appropriate mechanical means, such as fans or extractors, located at one end of the furnace.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Ceramic Engineering (AREA)
  • Materials Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • General Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Structural Engineering (AREA)
  • Organic Chemistry (AREA)
  • Baking, Grill, Roasting (AREA)
  • Muffle Furnaces And Rotary Kilns (AREA)
  • Furnace Details (AREA)
  • Tunnel Furnaces (AREA)
  • Chemical And Physical Treatments For Wood And The Like (AREA)

Description

DOMAINE TECHNIQUETECHNICAL AREA

L'invention concerne un four à feu tournant pour la cuisson des produits carbonés et notamment des anodes carbonées utilisées pour la production d'aluminium par électrolyse selon le procédé Hall-Héroult.The invention relates to a rotary kiln for cooking carbonaceous products and in particular carbon anodes used for the production of aluminum by electrolysis according to the Hall-Héroult process.

ETAT DE LA TECHNIQUESTATE OF THE ART

Les fours à feu tournant, tels que celui décrit dans la demande européenne EP-A-0 541 165, comportent généralement 2 rangées parallèles de chambres juxtaposées de forme rectangulaire dans lesquelles s'effectue la cuisson des anodes ou autres produits carbonés crus. Ces chambres, séparées par des murs transversaux, et dont le fond et les cloisons latérales sont isolées thermiquement par un briquetage isolant, sont subdivisées en plusieurs compartiments ou alvéoles contenant les produits à cuire. Ces alvéoles sont séparées par des cloisons creuses à parois minces disposées parallèlement au grand axe du four. Dans ces cloisons creuses circulent des gaz chauds, dont la température peut atteindre 1150 voire 1200°C. Ils sont formés pour l'essentiel par les gaz de combustion engendrés par une ou plusieurs rampes de brûleurs que l'on déplace d'une chambre vers la suivante au fur et à mesure que la cuisson s'effectue.Rotating fire furnaces, such as that described in the European patent application EP-A-0 541 165, generally comprise two parallel rows of juxtaposed rectangular-shaped chambers in which anodes or other green carbonaceous products are fired. These rooms, separated by transverse walls, and whose bottom and side walls are thermally insulated by an insulating brickwork, are subdivided into several compartments or cells containing the products to be cooked. These cells are separated by thin-walled hollow partitions arranged parallel to the major axis of the furnace. In these hollow partitions circulate hot gases, whose temperature can reach 1150 or 1200 ° C. They are formed essentially by the combustion gases generated by one or more burner ramps that are moved from one chamber to the next as the cooking takes place.

On distingue souvent parmi les fours à feu tournant, les fours à chambres de type ouvert et les fours à chambres de type fermé. La différence réside principalement dans les caractéristiques constructives du briquetage intérieur conduisant à divers cheminements des gaz chauds en circulation autour des alvéoles contenant les charges à cuire, mais l'organisation générale de ces fours à feu tournant reste la même avec l'existence de 2 rangées de chambres parallèles, dont la longueur peut atteindre près de 200 mètres, reliées à leurs extrémités par des carneaux.Rotating furnaces, open-type furnaces and closed-type furnaces are often distinguished. The difference lies mainly in the constructive characteristics of the interior brickwork leading to various paths of the hot gases circulating around the cells containing the loads to be cooked, but the general organization of these rotary kilns remains the same with the existence of 2 rows parallel rooms, whose length can reach nearly 200 meters, connected at their ends by flues.

Ces rangées de chambres parallèles isolées thermiquement sur 3 faces (isolations latérales + fond) sont contenues dans un cuvelage en béton formé d'un radier horizontal ou fond de cuve et de 2 murs ou voiles verticaux latéraux. A ce stade 2 modes de construction sont possibles avec leurs avantages et leurs inconvénients respectifs en mettant en oeuvre :

  • soit un cuvelage unique renfermant les 2 rangées de chambres et leurs isolations; configuration souvent adoptée pour les fours à chambres de type fermé;
  • soit un cuvelage double, chaque cuvelage renfermant une rangée de chambres; configuration souvent adoptée pour les fours à chambres de type ouvert.
These rows of parallel chambers thermally insulated on 3 sides (lateral insulation + bottom) are contained in a concrete casing formed of a horizontal slab or bottom of tank and 2 walls or lateral vertical sails. At this stage, two modes of construction are possible with their respective advantages and disadvantages by implementing:
  • a single casing containing the 2 rows of chambers and their insulation; configuration often adopted for closed chamber furnaces;
  • a double casing, each casing enclosing a row of chambers; configuration often adopted for open type ovens.

Il s'agit là d'une différence constructive importante mais qui n'est pas liée au type de fours à chambres; en d'autres termes, un four de type fermé à double cuvelage est tout à fait réalisable au même titre qu'un four de type ouvert à cuvelage unique.This is a significant constructive difference but not related to the type of room ovens; in other words, a double-cased closed type furnace is entirely feasible as is a single casing open type furnace.

L'avantage du cuvelage unique est sa grande compacité et donc le gain de place qui en résulte ainsi que l'économie qu'il entraîne sur le plan des coûts d'investissements, mais ceci au détriment de la bonne tenue et donc de la longévité des briquetages isolants qui sont disposés entre les 2 rangées de chambres. En effet ces briquetages supportent des contraintes thermiques et mécaniques importantes du fait de l'amplitude des variations de température auxquelles ils sont soumis et des poussées exercées par les chambres situées de part et d'autre de ces briquetages. En raison des difficultés d'assurer un refroidissement efficace de cette zone centrale, le refroidissement du cuvelage unique se limite dans la plupart des fours industriels à cuvelage unique à une simple ventilation naturelle des murs ou voiles extérieurs du cuvelage. Ce traitement thermique différencié de la zone centrale par rapport aux zones extérieures engendre de surcroît des contraintes mécaniques et thermiques créées par le gradient thermique élevé existant entre les chambres en vis à vis situées dans chacune des 2 rangées de chambres constituant le four.The advantage of the unique casing is its great compactness and therefore the resulting saving of space as well as the savings it entails in terms of investment costs, but this to the detriment of good performance and therefore longevity insulating briquetting which is arranged between the 2 rows of rooms. Indeed, these briquetting bear significant thermal and mechanical stresses due to the amplitude of the temperature variations to which they are subjected and thrusts exerted by the chambers located on either side of these briquetting. Due to the difficulties of ensuring effective cooling of this central zone, the cooling of the single casing is limited in most single-cased industrial furnaces to a simple natural ventilation of the walls or outer walls of the casing. This differential heat treatment of the central zone with respect to the outer zones also generates mechanical and thermal stresses created by the high thermal gradient existing between the chambers facing each other in the two rows of chambers constituting the furnace.

L'avantage majeur de la cuve double est que la charge constituée par la rangée de chambres, est traitée de manière symétrique par rapport à son axe longitudinal. En particulier les voiles intérieurs sont refroidis comme les voiles extérieurs dans le cas le plus fréquent où il y a une ventilation naturelle assurée notamment par des canaux de circulation ou voûtains qui refroidissentr le fond du four. Cette configuration permet donc de prolonger la durée de vie des briquetages avec toutefois les inconvénients d'un coût de réalisation plus élevé et d'un plus grand encombrement au sol à capacité de production identique.The major advantage of the double bowl is that the load constituted by the row of chambers, is treated symmetrically with respect to its longitudinal axis. In particular the inner sails are cooled like the outer sails in the most frequent case where there is a natural ventilation provided in particular by the circulation channels or vaults which cool the bottom of the oven. This configuration therefore makes it possible to extend the lifetime of the briquetting, with, however, the disadvantages of a higher realization cost and a larger footprint with identical production capacity.

PROBLEME POSEPROBLEM

La réalisation d'un four à chambres pour la cuisson des produits carbonés présentant simultanément les avantages des fours à cuvelage unique et à cuvelage double à savoir : d'une part un encombrement limité et un coût de réalisation modéré, d'autre part une grande longévité des briquetages notamment des briquetages centraux, demeure un problème mal résolu pour le constructeur ou l'utilisateur de four à feu tournant.The production of a chamber oven for cooking carbon products simultaneously presenting the advantages of single-cased and double-cased furnaces, namely: on the one hand a limited space requirement and a moderate production cost, on the other hand a large longevity of brickwork including central briquetting, remains a problem poorly resolved for the builder or the user of a rotating furnace.

OBJET DE L'INVENTIONOBJECT OF THE INVENTION

L'invention apporte une solution à ce problème. Elle concerne plus précisément un four à feu tournant pour la cuisson de produits carbonés comportant notamment 2 rangées parallèles de chambres de cuisson placées avec leur propre isolation thermique conjointement ou séparément dans un cuvelage, de préférence en béton, refroidi au moins par ventilation de ses murs latéraux extérieurs ou voiles extérieurs caractérisé en ce que les 2 rangées parallèles de chambres de cuisson sont séparées par un voile intérieur qui est refroidi spécifiquement et rendu solidaire du fond du cuvelage ou radier.The invention provides a solution to this problem. It relates more specifically to a rotary fired furnace for cooking carbon products including in particular 2 parallel rows of cooking chambers. placed with their own thermal insulation jointly or separately in a casing, preferably made of concrete, at least cooled by ventilation of its external lateral walls or external walls, characterized in that the 2 parallel rows of cooking chambers are separated by an internal veil which is specifically cooled and made integral with the bottom of the casing or write off.

Ce voile intérieur, dont l'épaisseur varie notamment en fonction de la nature des matériaux utilisés pour sa construction, comporte un réseau de conduits verticaux, horizontaux ou de toute autre géométrie autorisant la circulation d'un fluide refroidisseur liquide ou gazeux, permettant d'abaisser la température du ou des matériaux constitutifs du voile central à une valeur acceptable par lesdits matériaux. De préférence le voile intérieur est formé par 2 montants verticaux d'épaisseur identique, symétriques par rapport à l'axe vertical de symétrie, liés à leurs extrémités inférieures au fond du cuvelage ou radier. Ces montants sont maintenus à écartement fixe par des entretoises verticales ou horizontales de manière à créer des couloirs verticaux ou horizontaux dans lesquels circule le fluide refroidisseur, qui est de préférence de l'air de ventilation fourni par des moyens de ventilation appropriés. En général les entretoises sont constituées du même matériau que les montants verticaux.This internal web, the thickness of which varies in particular according to the nature of the materials used for its construction, comprises a network of vertical, horizontal ducts or any other geometry allowing the circulation of a coolant liquid or gaseous, allowing lowering the temperature of the constituent material (s) of the central web to an acceptable value by said materials. Preferably the inner web is formed by 2 vertical uprights of identical thickness, symmetrical with respect to the vertical axis of symmetry, linked to their lower ends at the bottom of the casing or raft. These amounts are maintained at fixed spacing by vertical or horizontal spacers so as to create vertical or horizontal corridors in which circulates the cooling fluid, which is preferably ventilation air supplied by appropriate ventilation means. In general, the spacers are made of the same material as the vertical uprights.

Par moyens de ventilation appropriés, il faut comprendre aussi bien des moyens de ventilation naturelle, de ventilation forcée ou de ventilation mixte. Ces moyens de ventilation sont regroupés avec les autres moyens auxiliaires indispensables à la conduite du four, notamment moyens de contrôle et de régulation et moyens de levage et de manutention, dans le bâtiment qui abrite le four.Suitable means of ventilation include natural ventilation, forced ventilation or mixed ventilation. These ventilation means are grouped together with the other auxiliary means essential for driving the oven, including control and regulation means and lifting and handling means, in the building that houses the oven.

DESCRIPTIONDESCRIPTION

L'invention sera mieux comprise par la description détaillée ci-après illustrée par les figures suivantes :

  • . Fig.1 représentation schématique en vue de dessus d'un four à feu tournant à cuvelage double selon l'art antérieur.
  • . Fig.2 représentation schématique en coupe transversale selon B,B' du four à cuvelage double de la fig.1 selon l'art antérieur.
  • . Fig.3 représentation schématique en coupe transversale d'un four à cuvelage unique selon l'art antérieur.
  • . Fig.4 représentation schématique en coupe transversale d'un four à feu tournant avec un voile interne ventilé selon l'invention.
  • . Fig.5 représentation en perspective coupée du voile interne ventilé.
The invention will be better understood from the following detailed description illustrated by the following figures:
  • . Fig.1 schematic representation in plan view of a rotating furnace with double casing according to the prior art.
  • . Fig.2 schematic cross-sectional representation according to B, B 'of the double casing furnace of Fig.1 according to the prior art.
  • . Fig.3 schematic cross-sectional representation of a single casing furnace according to the prior art.
  • . Fig.4 schematic cross-sectional representation of a rotating furnace with a ventilated internal web according to the invention.
  • . Fig.5 cutaway perspective representation of the ventilated internal web.

La figure 1 est représentative d'un four à feu tournant 1 comportant 2 rangées parallèles 2a et 2b de chambres 3 juxtaposées de forme rectangulaire séparées par des murs transversaux 4 et subdivisées en alvéoles 5 contenant le produit à cuire. Ces alvéoles sont séparées par des cloisons creuses 6 à parois minces parallèles au grand axe A,A' du four dans lesquelles circulent les gaz destinés à chauffer les charges (non représentées) placées dans les alvéoles. Ces gaz chauds sont principalement des gaz de combustion engendrés par une ou plusieurs rampes 7 de brûleurs que l'on déplace d'une chambre vers la suivante au fur et à mesure que la cuisson du produit s'effectue.FIG. 1 is representative of a rotary firing furnace 1 comprising two parallel rows 2a and 2b of juxtaposed chambers 3 of rectangular shape separated by transverse walls 4 and subdivided into cells 5 containing the product to be fired. These cells are separated by hollow partitions 6 with thin walls parallel to the major axis A, A 'of the furnace in which circulate the gases for heating the charges (not shown) placed in the cells. These hot gases are mainly combustion gases generated by one or more ramps 7 of burners that are moved from one chamber to the next as the cooking of the product takes place.

Selon la figure 2 les 2 cuvelages en béton 8a et 8b contiennent respectivement les chambres 3a et 3b avec leur isolation thermique 17a et 17b. Les voiles extérieurs 9a et 9b ainsi que les 2 voiles intérieurs 10a et 10b des 2 cuvelages sont refroidis par ventilation naturelle ainsi que les 2 radiers 12a et 12b équipés de voûtains 11a et 11b. La distance entre les 2 faces externes des voiles intérieurs est de l'ordre de 2 à 3 mètres pour permettre une aération suffisante des 2 cuvelages par tirage naturel.According to Figure 2 the 2 concrete casings 8a and 8b respectively contain the chambers 3a and 3b with their thermal insulation 17a and 17b. The external sails 9a and 9b as well as the 2 inner sails 10a and 10b of the two casings are cooled by natural ventilation as well as the 2 rafts 12a and 12b equipped with vaults 11a and 11b. The distance between the 2 outer faces of the inner sails is of the order of 2 to 3 meters to allow sufficient ventilation of the two casings by natural draft.

Selon la figure 3, les 2 rangées parallèles 2a et 2b de chambres 3a, 3b sont contenues avec leur isolation thermique respective 17a et 17b dans un cuvelage unique 8 en béton formé par 2 voiles verticaux extérieurs 9a, 9b reposant sur un radier 12 en béton. Dans cette configuration la fréquence des interventions de maintenance sur les briquetages centraux est beaucoup plus élevée que celle constatée pour les briquetages de chambres ayant leur cuvelage individuel ce qui, indépendamment du coût direct d'entretien plus élevé, peut conduire à une limitation de la capacité de production.According to FIG. 3, the two parallel rows 2a and 2b of chambers 3a, 3b are contained with their respective thermal insulation 17a and 17b in a single casing 8 of concrete formed by 2 outer vertical sails 9a, 9b resting on a concrete base 12 . In this configuration the frequency of maintenance interventions on the central brickwork is much higher than that observed for brickwork of rooms having their individual casing which, independently of the direct cost of higher maintenance, can lead to a limitation of the capacity. of production.

A noter en revanche qu'à capacité de production égale, la réduction de largeur d'environ 3 mètres d'un four à cuvelage unique par rapport à un four à cuvelage double permet une diminution de surface d'occupation au sol de 300 à 600 m2 suivant la longueur du four.Note however that with equal production capacity, the width reduction of about 3 meters of a single casing kiln compared to a double casing furnace allows a reduction in floor area of 300 to 600 m 2 according to the length of the oven.

Selon les figures 4 et 5 représentatives d'un four à feu tournant à voile central ventilé de l'invention, on interpose entre les isolations thermiques 17a et 17b des chambres 3a et 3b, et plus précisément entre les briquetages centraux, un voile central vertical ou voile intérieur 10, de préférence en béton, dont l'épaisseur totale varie en fonction de la capacité du four et plus précisément de l'importance des flux thermiques à évacuer, mais aussi de la nature du matériau utilisé et notamment de ses propriétés thermomécaniques, résistances à l'écrasement et au choc thermique, conductibilité thermique ... Ce voile 10 a une épaisseur totale dans ses parties centrale et supérieure comprise entre 200 et 900 mm et de préférence entre 400 et 600 mm. Il s'élargit en général progressivement à sa base en appui sur le fond de cuvelage ou radier 12. Le voile 10, réalisé la plupart du temps en béton identique à celui du cuvelage 8, est formé de préférence par 2 montants verticaux 13 et 13b d'épaisseur identique, symétriques par rapport à l'axe vertical CC'. Ces montants 13a, 13b solidaires à leurs extrémités inférieures 14a, 14b du radier 12, sont maintenues à écartement constant "e" par des entretoises de préférence verticales ou horizontales 15 de section rectangulaire de 2 à 10 dm2 placées à espacement régulier entre les 2 montants pour en limiter la déformation, mais aussi pour former des couloirs 16 verticaux ou horizontaux communiquant à leurs extrémités avec des moyens de ventilation non représentés, ladite ventilation pouvant être naturelle, forcée ou mixte.According to FIGS. 4 and 5, representative of a ventilated central fan rotating firing furnace of the invention, there are interposed between the thermal insulators 17a and 17b of the chambers 3a and 3b, and more precisely between the central briquetting, a vertical central veil. or inner sail 10, preferably made of concrete, the total thickness of which varies according to the capacity of the furnace and more precisely the importance of the thermal flows to be evacuated, but also the nature of the material used and in particular its thermomechanical properties , crush and thermal shock resistance, thermal conductivity ... This web 10 has a total thickness in its central and upper parts of between 200 and 900 mm and preferably between 400 and 600 mm. It generally widens gradually to its base resting on the casing floor or base 12. The veil 10, made mostly of concrete identical to that of the casing 8, is preferably formed by 2 uprights vertical 13 and 13b of identical thickness, symmetrical with respect to the vertical axis CC '. These uprights 13a, 13b secured to their lower ends 14a, 14b of the slab 12, are kept at constant spacing "e" by spacers preferably vertical or horizontal 15 of rectangular section of 2 to 10 dm 2 placed at a regular spacing between the 2 amounts to limit the deformation, but also to form vertical or horizontal corridors 16 communicating at their ends with unrepresented ventilation means, said ventilation being natural, forced or mixed.

L'écartement entre 2 cloisons définies par les entretoises verticales ou horizontales 15 est compris entre 50 et 500 mm, mais de préférence entre 100 et 300 mm, de manière à assurer une ventilation suffisante dans un volume minimum. Quant à l'espacement des entretoises 15, il est déterminé en fonction des contraintes de déformation auxquelles sont soumises lesdits montants sous l'effet notamment des charges et de la température. Cet espacement est le plus souvent compris entre 0,5 et 1 mètre.The spacing between two partitions defined by the vertical or horizontal spacers 15 is between 50 and 500 mm, but preferably between 100 and 300 mm, so as to provide sufficient ventilation in a minimum volume. As for the spacing of the spacers 15, it is determined according to the deformation stresses to which said amounts are subjected under the effect of particular charges and temperature. This spacing is most often between 0.5 and 1 meter.

Selon cette configuration nouvelle, le voile intérieur 10 refroidi et d'épaisseur limitée n'entraîne donc pas, toutes choses égales par ailleurs, d'élargissement important du four à feu tournant, comme c'est le cas avec le four à double cuvelage. En revanche, étant refroidi naturellement, ou de façon forcée par ventilation d'air, ou par tout autre fluide refroidisseur, il permet de recréer la symétrie mécanique et thermique qui fait défaut à la cuve unique.According to this new configuration, the inner sail 10 cooled and limited thickness therefore does not lead, all things being equal, significant expansion of the furnace rotating, as is the case with the double-casing furnace. On the other hand, being cooled naturally, or forcibly by ventilation of air, or by any other cooling fluid, it makes it possible to recreate the mechanical and thermal symmetry that is lacking in the single vessel.

Le choix du mode de ventilation dépend principalement de l'importance du flux thermique à évacuer de la zone centrale du four pour limiter les pointes de température dans le briquetage. Pour un four de grande capacité, il y aura avantage à mettre en oeuvre un groupe de ventilation forcée suffisamment puissant pour injecter de l'air frais, de préférence du bas vers le haut des couloirs 16 verticaux du voile intérieur 10, éventuellement par l'intermédiaire des voûtains 11 du radier, et cela en conservant pour les voiles extérieurs 9a, 9b, une ventilation naturelle.The choice of the ventilation mode depends mainly on the importance of the heat flow to be removed from the central zone of the oven to limit the temperature peaks in the brickwork. For a large capacity oven, it will be advantageous to use a forced ventilation unit powerful enough to inject fresh air, preferably from the bottom to the top of the vertical corridors 16 of the inner veil 10, possibly by the intermediate of the vaults 11 of the raft, and this while maintaining for the outer sails 9a, 9b, a natural ventilation.

La ventilation forcée peut être réalisée aussi par injection d'air frais dans les couloirs 16 horizontaux, c'est-à-dire longitudinalement d'une extrémité du voile intérieur 10 à l'autre extrémité. L'injection d'air frais par soufflage ou aspiration est effectuée à l'aide de moyens mécaniques appropriés, tels que ventilateurs ou extracteurs, situés à une extrémité du four.Forced ventilation can also be performed by injecting fresh air into the horizontal corridors 16, that is to say longitudinally from one end of the inner web 10 to the other end. The injection of fresh air by blowing or aspiration is carried out using appropriate mechanical means, such as fans or extractors, located at one end of the furnace.

EXEMPLES D'APPLICATIONEXAMPLES OF APPLICATION

Pour les avantages cumulés précédemment énumérés, ce nouveau concept de four à feu tournant s'applique évidemment à la construction de fours neufs qu'ils soient ouverts ou fermés, mais il trouve aussi des applications intéressantes dans la transformation de fours existants dont il convient d'améliorer les performances à l'occasion d'une rénovation.For the cumulative advantages previously enumerated, this new concept of rotary kiln obviously applies to the construction of new furnaces whether open or closed, but it also finds interesting applications in the transformation of existing furnaces which are suitable for improve performance during a renovation.

Ainsi, dans le cas d'un four ouvert à double cuvelage à rénover, on peut aisément, à encombrement au sol constant, raccorder les 2 radiers 12a, 12b et rapprocher les 2 voiles internes 10a et 10b qui font alors fonction de montants 13a et 13b en conservant simplement un espacement suffisant pour former une cheminée 16 de circulation d'air communiquant à sa partie inférieure avec les voûtains existants 11. On peut ainsi augmenter la largeur des 2 rangées de chambres de 1 à 2 mètres et par suite augmenter le volume de la charge à cuire de 10 à 20%.Thus, in the case of an open double casing furnace to be renovated, it is easy, with constant floor space, to connect the two rafts 12a, 12b and bring together the two internal walls 10a and 10b which then act as uprights 13a and 13b simply by maintaining a spacing sufficient to form an air flow chimney 16 communicating at its lower part with the existing vaults 11. It is thus possible to increase the width of the 2 rows of chambers by 1 to 2 meters and consequently to increase the volume of the cooking load of 10 to 20%.

De même dans le cas d'un four fermé à cuvelage unique que l'on veut transformer en four ouvert par exemple pour en augmenter la capacité. Il est possible de réaliser cet objectif sans accroître l'encombrement au sol en appliquant le concept de l'invention qui consiste ici à interposer un voile ventilé interne 10 de 400 à 600 mm d'épaisseur, lié au radier 12 selon l'invention. Le voile central n'occupant qu'une partie très limitée du volume utile apporté par le cuvelage du four fermé, on bénéficie totalement de l'augmentation de capacité de production procurée par le four ouvert grâce à son meilleur rapport volume charge à cuire/volume briquetage et cela à encombrement au sol constant.Similarly, in the case of a single closed casing oven that is to be converted into an open oven for example to increase the capacity. It is possible to achieve this objective without increasing the footprint by applying the concept of the invention which is here to interpose an internal ventilated web 10 from 400 to 600 mm thick, connected to the base 12 of the invention. Since the central veil occupies only a very limited part of the useful volume provided by the closed oven casing, the production capacity provided by the open oven is fully benefited by its better load / cook volume ratio. bricklaying and this at constant ground congestion.

Claims (10)

  1. Baking ring furnace (1) used to bake carbonaceous compounds made notably of two parallel rows (2a, 2b) of baking chambers (3a, 3b) placed with their own thermal insulation (17a, 17b) jointly or separately in a basin 8, usually made of cement, cooled at least by ventilation of its two exterior walls or partitions (9a, 9b) characterized by the fact that the two parallel rows (2a, 2b)of baking chambers (3a, 3b) are separated by a unique interior partition (10) which is specifically cooled and made firmly attached to the bottom of the basin (12), and that the cooled interior partition (10) comprises a network of vertical, horizontal or any other geometric shape ducts or passages (16) allowing the circulation of a cooling liquid or gaseous fluid.
  2. Baking ring furnace according to claim 1 characterized by the fact that the interior partition (10) is made of two vertical members (13a, 13b) of identical thickness, symmetrical compared to the vertical axis CC', attached at their lower ends (14a, 14b) to the bottom of the basin (12) and maintained at a fixed spacing "e" by vertical or horizontal spacers (15) placed at fixed intervals in order to create vertical or horizontal passages (16).
  3. Baking ring furnace according to claim 2 characterized by the fact that the interior partition (10) has a total width in its central and higher parts comprising between 200 and 900 mm and preferably 400 and 600 mm.
  4. Baking ring furnace according to claim 2 characterized by the fact that the spacing "e" between the two members (13a, 13b) is 50 mm <e<500 mm and preferably 100 mm ≤ e ≤300 mm.
  5. Baking ring furnace according to claim 2 characterized by the fact that the regular space between the spacers (15) is between 0.5 and 1 meter.
  6. Baking ring furnace according to claim 2 characterized by the fact that the members (13a, 13b) are made of the same cement as the basin (8).
  7. Baking ring furnace according to any of claims 1 to 6 characterized by the fact that the cooling of the interior partition (10) is insured by circulation of air in the passages (16) communicating at their ends with natural ventilation means, forced or mix.
  8. Baking ring furnace according to claims 1 or 7 characterized by the fact that the forced ventilation is realized by injection of cool air, from the bottom to the top of the vertical passages (16) of the interior partition (10), optionally using the ventilation ducts (11) of the basin whereas the exterior walls (9a, 9b) are cooled by natural ventilation.
  9. Baking ring furnace according to claims 1 or 7 characterized by the fact that the forced ventilation is realized by injection of cool air, longitudinally from one end of the interior partition (10) to the other, in the horizontal passages (16).
  10. Baking ring furnace according to claim 9, characterized by the fact that the forced ventilation is done by blowing or aspiration of cool air using appropriate mechanical means situated at one end of the furnace.
EP96901839A 1995-01-27 1996-01-23 Firing furnace with a revolving firing zone and a cooled internal wall Expired - Lifetime EP0760076B2 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
FR9501186 1995-01-27
FR9501186A FR2730045A1 (en) 1995-01-27 1995-01-27 ROTATING FIRE COOKING OVEN WITH COOLED INNER SHEET
PCT/FR1996/000112 WO1996023186A1 (en) 1995-01-27 1996-01-23 Firing furnace with a revolving firing zone and a cooled internal wall

Publications (3)

Publication Number Publication Date
EP0760076A1 EP0760076A1 (en) 1997-03-05
EP0760076B1 EP0760076B1 (en) 2000-04-19
EP0760076B2 true EP0760076B2 (en) 2007-06-06

Family

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EP96901839A Expired - Lifetime EP0760076B2 (en) 1995-01-27 1996-01-23 Firing furnace with a revolving firing zone and a cooled internal wall

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EP (1) EP0760076B2 (en)
AR (1) AR000818A1 (en)
AU (1) AU696043B2 (en)
BR (1) BR9603960A (en)
CA (1) CA2184410C (en)
FR (1) FR2730045A1 (en)
NO (1) NO311991B1 (en)
WO (1) WO1996023186A1 (en)

Families Citing this family (2)

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Publication number Priority date Publication date Assignee Title
FR2730045A1 (en) 1995-01-27 1996-08-02 Pechiney Aluminium ROTATING FIRE COOKING OVEN WITH COOLED INNER SHEET
WO2013187960A1 (en) * 2012-06-15 2013-12-19 Fluor Technologies Corporation Carbon baking oxygen preheat and heat recovery firing system

Citations (1)

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Publication number Priority date Publication date Assignee Title
US5779970A (en) 1995-01-27 1998-07-14 Aluminium Pechiney Convection cooking oven with a cooled interior

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB241303A (en) * 1924-07-23 1925-10-22 Duncan Whitehouse Improvements in or relating to brick kilns
US3975149A (en) * 1975-04-23 1976-08-17 Aluminum Company Of America Ring furnace
DE2519738C2 (en) * 1975-05-02 1986-09-18 Ludwig Riedhammer GmbH, 8500 Nürnberg Process for burning carbon bodies, such as electrodes or carbon stones, as well as ring furnace for carrying out the process
IT1073727B (en) * 1976-05-05 1985-04-17 Elettrocarbonium Spa IMPROVEMENT IN CONTINUOUS RING OVENS FOR COOKING OR ANNEALING OF CARBON MATERIALS
US4266316A (en) * 1979-09-21 1981-05-12 Ardal Og Sunndal Verk A.S. Suction tube assembly for ring furnace
NO152029C (en) * 1982-11-05 1985-07-17 Ardal Og Sunndal Verk RING ROOM OVEN AND PROCEDURE FOR OPERATING THIS
US4687439A (en) * 1986-02-28 1987-08-18 Aluminum Company Of America & Delta Refractories, Inc. Furnaces for baking anodes
US4842511A (en) * 1987-12-28 1989-06-27 Aluminum Company Of America Carbon baking furnace--refractory construction
NO174364C (en) * 1991-11-06 1994-04-20 Norsk Hydro As Device by ring chamber oven

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5779970A (en) 1995-01-27 1998-07-14 Aluminium Pechiney Convection cooking oven with a cooled interior

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
Dessin industriel "Dispositionsplan, Ofen Nr. 1" (Disposition générale, four No 1) No 59.0.00164 de la société Riedhammer Industrieoefen daté du 15.09.78
Dessin industriel "Fundamentplan" (Plan des fondations) No 59.0. 00009 b de la société Ludwig Riedhammer GmbH daté du 28.02.77
J. Auton, W.F. Crowell, R.R. Ebersole, W.W. Ellison, J. Kaiser, J.G. Peacey, E.J. Chin, "Noranda anode baking Furnace - Design and performance",exposés des sessions techniques tenues lors du 113ème rencontres annuelles de Light Metals, Los Angeles, Californie, USA, du 27 février au 1er mars 1984, une publication de "The metallurgical

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NO311991B1 (en) 2002-02-25
US5779970A (en) 1998-07-14
CA2184410A1 (en) 1996-08-01
WO1996023186A1 (en) 1996-08-01
NO963484L (en) 1996-08-21
CA2184410C (en) 2003-07-15
AU4625996A (en) 1996-08-14
EP0760076B1 (en) 2000-04-19
EP0760076A1 (en) 1997-03-05
FR2730045A1 (en) 1996-08-02
AU696043B2 (en) 1998-08-27
FR2730045B1 (en) 1997-03-07
BR9603960A (en) 1997-10-07
AR000818A1 (en) 1997-08-06

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